Method for preparing high-quality pentaerythritol high-carbon fatty acid ester by adopting extraction process
A pentaerythritol and fatty acid ester technology, applied in the direction of fatty acid esterification, fatty acid production, fatty acid chemical modification, etc., can solve the problems of difficult layering of fatty acid sodium soap and ester, inability to carry out production operations, high product viscosity, etc. High point, small equipment investment, good heat resistance
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Embodiment 1
[0028] Embodiment 1: prepare the method for high-quality pentaerythritol high-carbon fatty acid ester with extraction process, the steps are as follows:
[0029] 1. Material selection: select high-carbon fatty acids with an acid value of 190-200 and an iodine value of 80-100, a purity of ≥98% pentaerythritol, and a purity of ≥99.5% of 200-mesh zinc powder; the proportioning composition of the above-mentioned raw materials is:
[0030] High carbon fatty acid 100kg
[0031] Pentaerythritol 12 kg
[0032] Zinc powder 0.5 kg;
[0033] ②Esterification: process conditions: the temperature of esterification reaction is controlled at 180-200°C,
[0034] Vacuum degree: ≤1000pa, reaction time 6 hours;
[0035] In a vacuum state, the water generated by esterification is vaporized and pumped out of the reactor. When the temperature of the esterification reaction rises to 210 ° C, the vacuum degree is ≤ 500 Pa, and the esterification reaction ends when no water vapor is drawn out;
[0...
Embodiment 2
[0039] Embodiment 2: prepare the method for high-quality pentaerythritol high-carbon fatty acid ester with extraction process, the steps are as follows:
[0040] 1. Material selection: select high-carbon fatty acids with an acid value of 190-200 and an iodine value of 80-100, a purity of ≥98% pentaerythritol, and a purity of ≥99.5% of 200-mesh zinc powder; the proportioning composition of the above-mentioned raw materials is:
[0041] High carbon fatty acid 110kg
[0042] Pentaerythritol 12 kg
[0043] Zinc powder 0.6 kg;
[0044] ②, Esterification: process conditions: the temperature of the esterification reaction is controlled at 210°C,
[0045] Vacuum degree: ≤1000pa, reaction time 7 hours;
[0046] In a vacuum state, the water generated by esterification is vaporized and pumped out of the reactor. When the temperature of the esterification reaction rises to 210 ° C, the vacuum degree is ≤ 500 Pa, and the esterification reaction ends when no water vapor is drawn out;
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